 |
OPCW |
Conference
of the States Parties |
| Seventh
Session |
C-7/DEC.13 |
| 7
- 11 October 2002 |
10
October 2002 |
| Original:
ENGLISH |
| (Unofficial
electronic version) |
|
|
|
|
|
|
DECISION
REQUEST
BY THE RUSSIAN FEDERATION FOR APPROVAL TO USE A CHEMICAL WEAPONS PRODUCTION
FACILITY (SOMAN PRODUCTION)
AT
OJSC “KHIMPROM”, VOLGOGRAD,
FOR
PURPOSES NOT PROHIBITED UNDER THE CONVENTION
The
Conference of the States Parties,
Upon
the recommendation of the Executive Council at its Twenty-First Meeting
(EC-M-21/DEC.3, dated 3 October 2002),
Considering
the specific information received from the Russian Federation on the equipment
to be installed outside the declared perimeter and therefore excluded from
the conversion request, as specified in the attachment to this document; and
Further
considering the specific information received from the Russian Federation
on certain equipment to be used within the converted facility, as well as
on certain equipment to be destroyed, as also specified in the attachment
to this document.
Hereby:
Approves
the request to use a soman production facility at OJSC “Khimprom” in Volgograd,
Russian Federation, for purposes not prohibited under the Convention.
Attachment
(English and Russian only):
Addendum
to request for conversion of a soman production facility (EC-XXVI/NAT.2, dated
17 August 2001)
ADDENDUM
TO REQUEST FOR
CONVERSION
OF A SOMAN PRODUCTION FACILITY
(EC-XXVI/NAT.2,
dated 17 August 2001)
The
Russian Federation is seeking to convert only the dichlordiphenylsulphone
production stage. Consequently, equipment used at other stages of production
is to be moved beyond the perimeter of the facility.
| Page
40, Form CWP5.12 |
In
the conversion request, delete the commercial equipment for producing
polyestersulphone (building 304a), which is to be moved beyond the perimeter
of the facility. A list of the commercial equipment for producing polyestersulphone
(building 304a) which is to be moved beyond the perimeter of the facility
is on pp. 2-3 hereof. |
The
clarifications to the list of standard equipment for producing dichlordiphenylsulphone,
required as a result of the exclusion of DDVF production from the request,
are indicated below. Equipment not in use will be dismantled and destroyed.
| Page
47 Form CWP5.12 |
Insert
into columns 5-6 details of the standard equipment which will be used
for producing dichlordiphenylsulphone (position numbers on the process
line) or destroyed. A list of the standard equipment is in the annex
on pp. 3-4 hereof. |
FORM CWP 5.12. General Facility
Conversion Plan: Equipment to be Used/Proposed to be Used in the Converted
Facility
| |
| PLEASE
CHECK ONE |
| At
EIF, the facility IS being (will be) used for purposes not prohibited
by the Convention Yes |
| At
EIF, the facility IS NOT being (will not be) used for purposes
not prohibited by the Convention ________ |
| |
| Standard
equipment |
Spare
parts for standard/specialised equipment (if applicable) |
| Type |
Number
of Items |
Volume,
m3 |
Material |
Type |
Number
of
items |
| 1 |
2 |
3 |
4 |
5 |
6 |
| Equipment
for the commercial production of polyestersulphone. Building 304a. (To
be moved beyond the declared perimeter of the facility) |
| 1
Collector E1 |
1 |
V=6.3
m3 |
Chrome-nickel
steel |
|
|
| 2
Pump H2 |
1 |
Q=12.5
m3/h |
Chrome-nickel
steel |
|
|
| 3
Vessel E3 |
1 |
V=2.5
m3 |
Steel,
enamel |
|
|
| 4
Reactor P4 |
1 |
V=3.2
m3 |
Chrome-nickel-
molybdenum steel |
|
|
| 5
Reactor P5 |
1 |
V=2.5
m3 |
Steel,
enamel |
|
|
| 6
Pump H6 |
1 |
Q=45
m3 |
Graphite |
|
|
| 7
Reactor P7 |
1 |
V=6.3
m3 |
Steel,
enamel |
|
|
| 8
Filter F8 |
1 |
F=1.5
m2 |
Chrome-nickel
steel |
|
|
| 9
Collector E9 |
2 |
V=1.6
m3 |
Steel,
enamel |
|
|
| 1
|
2 |
3 |
4 |
5 |
6 |
| 10
Pump H11 |
1 |
Q=45
m3/h |
Graphite |
|
|
| 11
Collector E10 |
1 |
V=6.3
m3 |
Steel,
enamel |
|
|
| 12
Heat exchanger T12 |
1 |
F=12.5
m2 |
Chrome-nickel-
molybdenum steel |
|
|
| 13
Collector E12a |
1 |
V=
0.125 m3 |
Steel,
enamel |
|
|
| 14
Dryer X13 |
1 |
V=1
m3, F=6 m2 |
Chrome-nickel
steel |
|
|
| 15
Heat exchanger T14 |
1 |
F=10
m2 |
Chrome-nickel
steel |
|
|
| 16
Container X16 |
1 |
V=0.63
m3 |
Chrome-nickel
steel |
|
|
| 17
Vacuum pump H18 |
1 |
Q=3
m3/min |
Chrome-nickel
steel |
|
|
| 18
Reactor P30 |
1 |
V=1.6
m3 |
Titanium |
|
|
| 19
Heat exchanger T311-2 |
2 |
F=12.5
m2 |
|
|
|
| 20
Dispersant H33 |
1 |
Q=6.3
m3/h |
Chrome-nickel
steel |
|
|
| 21
Filter F34 |
1 |
F=1.5
m2 |
Chrome-nickel
steel |
|
|
| 22Bunker
X351-2 |
2 |
V=1
m2 |
Chrome-nickel
steel |
|
|
| 23
Collector E36 |
1 |
V=1.6
m3 |
Steel,
enamel |
|
|
| 24
Pump H37 |
1 |
Q=6.3
m3/h |
Chrome-nickel
steel |
|
|
| 25
Dryer X38 |
1 |
V-1.6
m3, F=8 m2 |
Chrome-nickel
steel |
|
|
| 26
Heat exchanger T40 |
1 |
F=10
m2 |
Chrome-nickel
steel |
|
|
| 27Reactor
P451-2 |
2 |
V=3.2
m3 |
Steel,
enamel |
|
|
| 28
Filter F46 |
1 |
F=
1.5 m2 |
Chrome-nickel
steel |
|
|
| 29
Collector E47 |
1 |
V=2
m3 |
Steel,
enamel |
|
|
| 30
Pump H48 |
1 |
Q=6.3
m3/h |
Chrome-nickel
steel |
|
|
| 1 |
2 |
3 |
4 |
5 |
6 |
| 31
Collector E49 |
1 |
V=1
m3 |
Chrome-nickel
steel |
|
|
| 32
Rotary-film evaporator T51 |
1 |
F=
3.2 m2 |
Chrome-nickel
steel |
|
|
| 33
Heat exchanger T52 |
1 |
F=
16.5 m2 |
Chrome-nickel
steel |
|
|
| 34
Vacuum pump H52a |
1 |
Q=3
m3/min |
Chrome-nickel
steel |
|
|
| 35
Container X54 |
1 |
V=1
m3 |
Steel,
enamel |
|
|
| 36
Pump H551-2 |
2 |
Q=6.3
m3/h |
Chrome-nickel
steel |
|
|
| Commercial
Equipment |
| Type |
Quantity |
Volume,
m3 |
Material |
Position
on process line |
To
be destroyed |
| 1 |
2 |
3 |
4 |
5 |
6 |
| Standard
equipment for commercial production of DDVF, Building 304a**** |
| Vacuum
pump (0561-3) H3281-3 |
3 |
Q=12m3/min |
Chrome-nickel
steel |
H-154\1-2 |
1
unit to be destroyed |
| Collector
(057) E329 |
1 |
V=0.2m3 |
Carbon
steel |
|
to
be destroyed |
| Vacuum
pump (0621-2) H3321-2 |
2 |
Q=12m3/min |
Chrome-nickel
steel |
|
to
be destroyed |
| Collector
(0136) E333 |
1 |
V=2m3 |
Chrome-nickel-molybdenum
steel |
E-97 |
|
| Heat
exchanger (0138) T334 |
1 |
F=16m2 |
Carbon
steel |
T-79 |
|
| Collector
(0139) E335 |
1 |
V=2
m3 |
Chrome-nickel-molybdenum
steel |
E-60 |
|
| Pump
(01401-2) H3361-2 |
2 |
Q=20m3/h |
Assembly |
147/1-2 |
|
| Collector
(058) E330 |
1 |
V=2m3 |
Chrome-nickel-molybdenum
steel |
E62 |
|
| Steam
ejection system (0611-2) H3311-2 |
2 |
Q=32kg/h
|
Carbon
steel, cast iron |
|
to
be destroyed |
| Heat
exchanger (061a) T331a |
1 |
F=40m2 |
Carbon
steel |
T353
(conden-sate collection station) |
|
| Pump
(01411) H3371 |
1 |
Q=162m3/h |
Assembly |
H157/2 |
|
| Pump
(01412) H3372 |
1 |
Q=190m3/h |
Assembly |
H157\3 |
|
| Collector
(0142) E338 |
1 |
V=2m3 |
Carbon
steel |
E151 |
|
| Heat
exchanger (0143) T339 |
1 |
F=65m2 |
Chrome-nickel
steel |
T102 |
|
| Vessel
(054) E3431 |
1 |
V=5m3 |
Carbon
steel |
E162 |
|
| Vessel
(0105) E3432 |
1 |
V=2m3 |
Carbon
steel |
E146 |
|
|
|
|
|
|
|
|
|
|
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